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We describe an E. coli-based cell-free system for the production of proteins with a non-natural amino acid (nnAA) incorporated site-specifically (modified protein). The mutant Methanococcus jannaschii tyrosyl-tRNA synthetase (mTyrRS) and tRNA(Tyr) pair were used as orthogonal elements. The mTyrRS experienced proteolysis and modified protein yields improved with higher synthetase addition (200-300 microg/mL). Product yields were also improved by increasing levels of total protein to 20 mg protein/mL and available vesicle surface area to 0.5 m(2)/mL. This new E. coli-based cell-free procedure produced up to 400 microg/mL of eCAT109pAz, 660 microg/mL of eDHFR10pAz, and 210 microg/mL of mDHFR31pAz with p-azido-L-phenylalanine (pAz) incorporated site-specifically at the amber nonsense codon. O-methyl-L-tyrosine and p-acetyl-L-phenylalanine were incorporated by similar protocols. The desired specificity for incorporation of the nnAA by the cell-free system was confirmed. Additionally, the modified proteins were enzymatically active and reactive for copper(I)-catalyzed (3 + 2) cycloadditions (click chemistry).

Due to its small size and intense luminescent signal, Gaussia princeps luciferase (GLuc) is attractive as a potential imaging agent in both cell culture and small animal research models. However, recombinant GLuc production using in vivo techniques has only produced small quantities of active luciferase, likely due to five disulfide bonds being required for full activity. Cell-free biology provides the freedom to control both the catalyst and chemical compositions in biological reactions, and we capitalized on this to produce large amounts of highly active GLuc in cell-free reactions. Active yields were improved by mutating the cell extract source strain to reduce proteolysis, adjusting reaction conditions to enhance oxidative protein folding, further activating energy metabolism, and encouraging post-translational activation. This cell-free protein synthesis procedure produced 412mug/mL of purified GLuc, relative to 5mug/mL isolated for intracellular Escherichia coli expression. The cell-free product had a specific activity of 4.2x10(24)photons/s/mol, the highest reported activity for any characterized luciferase.

The use of cell-free protein synthesis (CFPS) for recombinant protein production is emerging as an important technology. For example, the openness of the cell-free system allows control of the reaction environment to promote folding of disulfide bonded proteins in a rapid and economically feasible format. These advantages make cell-free protein expression systems particularly well suited for producing patient specific therapeutic vaccines or antidotes in response to threats from natural and man-made biological agents and for pharmaceutical proteins that are difficult to produce in living cells. In this work we assess the versatility of modern cell-free methods, optimize expression and folding parameters, and highlight the importance of rationally designed plasmid templates for producing mammalian secreted proteins, fusion proteins, and antibody fragments in our E. coli-based CFPS system. Two unique CFPS platforms were established by developing standardized extract preparation protocols and generic cell-free reaction conditions. Generic reaction conditions enabled all proteins to express well with the best therapeutic protein yield at 710 microg/mL, an antibody fragment at 230 microg/mL, and a vaccine fusion protein at 300 microg/mL; with the majority correctly folded. Better yields were obtained when cell-free reaction conditions were optimized for each protein. Establishing general CFPS platforms enhances the potential for cell-free protein synthesis to reliably produce complex protein products at low production and capital costs with very rapid process development timelines., ((c) 2007 Wiley Periodicals, Inc.)

The primary objective of this work was to create a cell-free protein synthesis extract that produces proteins requiring disulfide bonds while using glucose as an energy source. We attempted to avoid using iodoacetamide (IAM) to stabilize the required oxidizing thiol redox potential, since previous IAM pretreatments prevented glucose utilization apparently by inactivating glyceraldehyde 3-phosphate dehydrogenase (G-3PDH). Instead, the glutathione reductase (Gor)-mediated disulfide reductase system was disabled by deleting the gor gene from the KC6 cell-extract source strain. The thioredoxin reductase (TrxB)-mediated system was disabled by first adding a purification tag to the trxB gene in the chromosome to create strain KGK10 and then by affinity removal of the tagged TrxB. This was expected to result in a cell extract devoid of all disulfide reductase activity, but this was not the case. Although the concentration of IAM required to stabilize oxidized glutathione in the KGK10 extract could be reduced 20-fold, IAM pretreatment was still required to avoid disulfide reduction. Nonetheless, active urokinase and murine granulocyte macrophage-colony stimulating factor (mGM-CSF) were produced in reactions with KGK10 extract either with affinity removal of TrxB or with 50 microM IAM pretreatment. With the less intensive IAM pretreatment, glucose could be used as an energy source in a production system that promotes oxidative protein folding. This new protocol offers an economically feasible cell-free system for the production of secreted mammalian proteins as human therapeutics or vaccines., ((c) 2006 Wiley Periodicals, Inc.)

Recombinant adenoviruses continue to be a leading vector choice for gene transfer applications, with growing interest in the use of less prevalent serotypes, and of chimeras. As a result, the development of scaleable purification processes for alternative serotypes is needed. Anion-exchange chromatography is routinely used for scaleable adenovirus type 5 purification; however, retention varies for other serotypes because of differences in the exposed capsid proteins. Understanding how the viral surface influences retention behavior can provide a rational basis for chromatography development and optimization. In this work, chimeric vectors were used to show that the hexon protein is responsible for retention differences in anion-exchange chromatography. Next, the relative retention of eight serotypes from three subgroups was studied. Although all serotypes bound to the anion-exchange resin, the sodium chloride required to elute the virus varied over a 2- fold range, from 270 to 490 mM. Retention was accurately correlated to the electrostatic properties of the hexon protein, with an average error in sodium chloride concentration required to elute of only 14 mM. This correlation enables preparative chromatography gradients for alternative serotypes to be established with minimal effort.

The use of recombinant adenoviral vectors for vaccination and gene therapy requires the development of purification processes that are cost-effective, scalable, and capable of robust host cell DNA clearance. An adenovirus purification process was developed which incorporates selective precipitation of host cell DNA, enabling a reduction in the use of costly nucleases and chromatographic resins while substantially improving DNA and protein clearance capabilities. In this work, three cationic detergents were evaluated for their capacity to selectively precipitate DNA from adenovirus-containing cell lysate. Parameters including pH, sodium chloride concentration, nonionic surfactant concentration, and cell density were investigated during development of the precipitation step. In a novel application, the cationic detergent domiphen bromide was found to have superior selectivity for host cell DNA. In addition, domiphen bromide-induced precipitation of adenovirus was shown to be reversible, which reduces the importance of mixing. Precipitation of DNA in the cell lysate coupled with primary clarification resulted in 3 logs of DNA clearance and improved impurity clearance in the subsequent ultrafiltration step. As a result, nuclease treatment and/or anion exchange chromatography can be eliminated, or included exclusively to improve process robustness.

Extracorporeal blood oxygenators are used to provide cardiopulmonary support during open heart surgery. In the study reported here, mass transfer correlations were determined for commercially available blood oxygenators. Two configurations used commercially, flow outside and across bundles of hollow fibers and flow in thin channels between parallel flat sheet membranes, were investigated. Water and glycerol/water mixtures were used as a substitute for blood. Diffusion of oxygen into and out of these solutions was studied. For flow across bundles of hollow fibers, the mass transfer correlations derived here are in agreement with analogous correlations for crossflow heat exchangers. However, for flow in thin channels, the rate of mass transfer is often less than predicted from theory. This compromised mass transfer can be explained by considering slight variations in the thickness of the blood flow channels. The mass transfer correlations developed here could be used to design better blood oxygenators.